CN101221023B - Heat transmission device - Google Patents
Heat transmission device Download PDFInfo
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- CN101221023B CN101221023B CN2008100040427A CN200810004042A CN101221023B CN 101221023 B CN101221023 B CN 101221023B CN 2008100040427 A CN2008100040427 A CN 2008100040427A CN 200810004042 A CN200810004042 A CN 200810004042A CN 101221023 B CN101221023 B CN 101221023B
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- Prior art keywords
- heat
- chamber
- structure layer
- wick
- transfer arrangement
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
- F28D15/0233—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes the conduits having a particular shape, e.g. non-circular cross-section, annular
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
- F28D15/04—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes with tubes having a capillary structure
- F28D15/046—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes with tubes having a capillary structure characterised by the material or the construction of the capillary structure
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2215/00—Fins
- F28F2215/10—Secondary fins, e.g. projections or recesses on main fins
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L2924/00—Indexing scheme for arrangements or methods for connecting or disconnecting semiconductor or solid-state bodies as covered by H01L24/00
- H01L2924/0001—Technical content checked by a classifier
- H01L2924/0002—Not covered by any one of groups H01L24/00, H01L24/00 and H01L2224/00
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T29/00—Metal working
- Y10T29/49—Method of mechanical manufacture
- Y10T29/4935—Heat exchanger or boiler making
- Y10T29/49353—Heat pipe device making
Abstract
A heat transfer device includes a base chamber (110), a fin chamber (120), and at least one fin (130). The chambers can be thermally coupled. The heat transfer device also includes a wick structure. The wick structure can include a multi-wick structure. The multi-wick structure can include a three dimensional wick structure and/or a spatially varying wick structure.
Description
The application is to be on May 15th, 2003 applying date, and application number is 03816747.6, and denomination of invention is divided an application for " vapor augmented heatsink with multicore structure " one Chinese patent application.
Technical field
The present invention relates to cooling device, particularly relate to the heat-transfer arrangement that steam strengthens.
Background technology
Because electronic component then improves constantly with device trend microminiaturization arithmetic speed, the heat that is produced becomes the major obstacle of the performance of improving electronic installation and system.Radiator is to be used for the fexible unit that dissipates the hot ambient from the device that produces heat.
In many application, the heat that electronic installation produced can be dispersed in the air through radiator and go.The development of radiator has become heat treated principal focal point in the electronic system.The performance of radiator can be characterized by entire thermal resistance.The low more representative cooling/heat transfer performance of resistance is high more.Thermal-conduction resistance and thermal-convection resistance can influence the entire thermal resistance of radiator.Thermal-conduction resistance characterizes radiator from the ability of propagating to the convection current surface with the heat of the contact point of thermal source.Usually, for example can adopt high conduction such as aluminium or copper material and let it have short heat conduction path and big cross-sectional area reduces thermal-conduction resistance.Thermal-convection resistance characterizes radiator to the surrounding environment heat dissipation capability with given air flow configuration.Usually, Design of for heat sinks let its convection current surface quantity as much as possible.
Because the steam of evaporation is carrying the heat of evaporating area and through condensation on condensing surface heat is being discharged, and therefore can adopt heat pipe to reduce thermal-convection resistance.For instance, adopted flat-plate heat pipe to reduce the diffusion thermal resistance of radiator substrate at present.In addition, radiating fin, the heat pipe of promptly arranging by array configuration, thermo-contact is carried out in itself and solid substrate, can at utmost reduce the thermal-conduction resistance along radiating fin like this.Flat-plate heat pipe can combine formation substrate and radiating fin with other heat pipe.
Summary of the invention
Heat-pipe radiator comprises radiator, and in this radiator, radiating fin and substrate can be interconnective heat pipe chambers.This heat-pipe radiator can directly contact with semiconductor chip, and the bottom of basal compartment is flexible heat conduction thin slice, contacts thereby provide with the good of surface of semiconductor chip.The interconnective chamber of heat-pipe radiator can be processed by ceramic material.This ceramic material can form the main body with loose structure, and an impermeable layer can cover this porous ceramic bodies.Ceramic material can be capillary wick more uniform interconnective pore structure is provided.In addition, heat-pipe radiator can be processed through hot pressing or sintering metal powder and Overmolded hot conducting polymer.This fin chamber can have aciculiform array structure type and carry out convective heat transfer.The heat-pipe radiator that interconnects the chamber that is used for semiconductor package can comprise the channel as wick structure.In having heat-pipe radiator taper, hollow aciculiform fin chamber array, can adopt the channel capillary wick.
The wick structure of this heat-pipe radiator wick structure with comparatively traditional heat pipe on function is different.Particularly, the steam in comparatively traditional heat pipe and liquid flow be one dimension normally, and in heat-pipe radiator steam and flow of liquid more near three-dimensional.Equally, the mass velocity of condensed fluid changes with the space in heat-pipe radiator, in comparatively traditional heat pipe, does not then change.So, can use the wick structure of improvement.Heat-pipe radiator with wick structure of improvement can further reduce its thermal resistance.
Vapor augmented heatsink has been considered the wick structure of the three-dimensional feature of steam and flow of liquid in the heat pipe chamber and has been adopted heat pipe chamber and solid convective elements to come to reduce thermal-convection resistance as far as possible through employing, thereby high hot property is provided.
Across the heat transfer rate of heat pipe chamber the thermal-conduction resistance of vapor augmented heatsink there is direct contribution.This heat transfer rate can be limited by steam flow rate and flow rate of liquid.Because the performance of heat pipe chamber is relevant with three dimensional fluid stream, so its internal structure can allow three-dimensional vapor stream and three-dimensional liquid stream.For flow of liquid, because this vapor augmented heatsink is used for the electronic market, so its heating (evaporation) district has high heat flux factor usually.The size of vapor augmented heatsink and have high heat flux factor, this two combination make generation need have the wick structure of high wicking power and the conception of enough lift can be provided with respect to device size.Usually, be difficult to obtain to keep the wick structure that high flow velocity can provide big lift again.Yet, in fact have only heating (evaporation) district to have the high wicking power factor, and along with more far this wicking power factor is more little apart from this thermal treatment zone.Particularly, occur when being condensate in heat flux and significantly reducing, and the high condensation flow velocity of needs just on condensate flocks together the evaporation position at place only.Therefore, for the power (for example, capillary force, viscous force and gravity) of balanced action on liquid better, wick structure can change along with the needs of space flow speed.And the liquid of condensation can flow back to evaporating area through a plurality of liquid flow paths of three-dimensional, thereby has shortened travel distance.These factors make in this wick structure, to use to have the variable capillary wick of variable wick structure and/or variable thickness.
With regard to three-dimensional vapor stream, steam need diffuse through the chamber.Usually, the cross sectional dimensions of vapor chamber should be enough big.Yet,, just require whole chamber size smaller for more convection current surface area is arranged.Therefore, thin wick layer can provide bigger vapor chamber indoor.Thickness with this wick layer of different wick structure can be in the position attenuation except evaporating area.For example, because condensate liquid scale of construction there is lower than the condensate liquid scale of construction near the position of evaporating area, this fin chamber can have thin wick structure.Therefore, thus through the two all takes into account the overall performance that can improve vapor augmented heatsink thermal-convection resistance and thermal-conduction resistance.
In addition, in order to reduce the entire thermal resistance of heat-pipe radiator, can adopt solid convective fins.Because the thickness or the size of solid convective fins are littler than the heat pipe chamber usually; Therefore can increase the total quantity on convection current surface through in structure, adopting solid radiating fin; And the lip-deep variations in temperature of these convection current is very little, thereby reduces thermal-convection resistance.In order to obtain the littler convection current of variations in temperature surface, at least one side of solid fin can with the heat pipe chamber thermo-contact.
Except internal operations, can construct the radiating fin of vapor augmented heatsink to such an extent that further reduce thermal-convection resistance.Particularly, for the radiator of prior art, the substrate of solid fin is used for being transmitted to the top to heat from the substrate of radiating fin.Thereby having increased airborne pressure drop and reduced air, the radiating fin of this canal structure eliminates hot ability.Yet in vapor augmented heatsink, heat can be walked from substrate transfer through the steam condensation, therefore, opening can be set on solid fin.These openings can reduce airborne pressure drop, and are similar to pin grid array or loose structure can increase convective heat transfer.
The chamber can utilize material removal technology to process, for example machining and edm; Perhaps utilize material deformation technology, for example punching press, drawing, casting, molded, folding, lamination, sintering or weld prefabricated parts; Other forming materials technology of perhaps utilizing the present technique field to be known.Wick structure on the inwall of this device can be processed (for example, utilize molding or utilize lamination) simultaneously with the chamber.In addition, the technology that wick structure present technique also capable of using field is known independently processes, and connection technology in for example adopting like the grid processed with wire, powder sintered, or has the powder of jointing material; Perhaps adopt forming materials technology, like plating or coating or porous foam moulding; Perhaps adopt material removal process, like machining or etching; Perhaps adopt the combination of the technology that the present technique field known.Solid convective elements can be processed in make-up room.In addition, this convective elements also can utilize forming materials technology independently to process for example casting, molding, punching press or machining, other forming materials or the excision technology that perhaps adopt the present technique field to be known.Thermally coupled between the convective elements of independently processing and the chamber can through with or be connected technology without the material of interfacial adhesion material and realize; For example soldering, brazing, welding, hot activation are bonding, sound activate bonding, pressure activation is bonding, stickiness is bonding, perhaps other technology of being known of present technique field.Can before the sealing of chamber, introduce hydraulic fluid in the chamber.And the condition in the chamber can allow hydraulic fluid on a temperature between its curing condition and the critical condition, to evaporate.
Usually, heat-transfer arrangement comprises at least one basal compartment, at least one fin chamber and at least one radiating fin.These chambers ability thermally coupleds also are suitable for keeping condensable steam.
The application of this heat-transfer arrangement can comprise following one or more characteristics.This heat-transfer arrangement can comprise the radiating fin that at least one is solid, this radiating fin can have at least one side and with at least one basal compartment and fin chamber thermo-contact.This radiating fin can be processed by heat conducting material.
This heat-transfer arrangement can comprise at least one steam channel.
This heat-transfer arrangement also can comprise wick structure.This wick structure can be made of one with the wall of chamber.In addition, this wick structure can be done to such an extent that separate with the wall of chamber.This wick structure can comprise multicore structure, three-dimensional wick structure or with the wick structure of spatial variations.
This multicore structure can comprise that at least one bridge-type wick structure is to provide a plurality of liquid flow paths.In addition, this multicore structure can comprise the combination of groove, grid, polymeric powder capillary wick or foam wick core.Perhaps, this multicore structure can comprise the combination of layer structure, list structure or bridge-type wick structure.Again perhaps, this multicore structure can comprise the wick structure with different porosities or different hole dimensions.This capillary wick can have different cross-sectional areas geometry and different yardsticks.
This wick structure can comprise the wick structure with spatial variations.Should can be the groove structure that has with the spatial variations pattern with the wick structure of spatial variations.
In addition, this wick structure can comprise polymeric powder capillary wick, foam wick core, at least one groove or mesh wick core.This wick structure can comprise layer structure.
This heat-transfer arrangement can comprise that further the wick structure that is suitable for storaging liquid adapts to liquid flow variation.
This heat-transfer arrangement further can comprise the wick structure between the relative wall that is installed in the chamber.
This heat-transfer arrangement can comprise that further at least one inner supporting structure prevents caving in of chamber.This inner supporting structure can comprise at least one solid parts.In addition, these inner supporting structure parts can comprise wick structure.
The radiating fin of this heat-transfer arrangement can comprise at least one opening.This opening can limit a plurality of geometries.In addition, this opening can also limit a plurality of yardsticks.
The radiating fin of this heat-transfer arrangement can comprise an opening that is positioned at airflow downstream portion.
The radiating fin of this heat-transfer arrangement can comprise the otch that is positioned on the side.This otch can limit a plurality of geometries.In addition, this otch can also limit a plurality of yardsticks.In addition, this otch can limit a slit.Have otch that side can with at least one thermo-contact in basal compartment and the fin chamber.
At least two radiating fins of this heat-transfer arrangement can comprise two interconnective radiating fins.These two interconnective radiating fins can connect through baffle plate.
This heat-transfer arrangement can also comprise at least one phase change element.
The chamber of this heat-transfer arrangement can form the shape of falling T-, two shape of falling T-, U-shape or W-shape.
Come the one or more embodiment of specific explanations below in conjunction with accompanying drawing and explanation.Can understand other characteristic better through specification and accompanying drawing and claims.
Description of drawings
Figure 1A is the three-dimensional view that has the vapor augmented heatsink of inverse-T-shaped heat pipe chamber.
Figure 1B be vapor augmented heatsink among Figure 1A along the cutaway view of A-A section, what illustrate is the diagrammatic sketch of an embodiment of mesh wick cored structure.
Fig. 1 C be vapor augmented heatsink among Figure 1A along the cutaway view of B-B section, what illustrate is another diagrammatic sketch of this embodiment of mesh wick cored structure among Figure 1B.
Fig. 2 A is the cutaway view of this embodiment of multicore wick structure along the A-A section, has special groove on the base plate of the vapor augmented heatsink of this structure in Figure 1A.
Fig. 2 B is the cutaway view of this embodiment of multicore wick structure along the B-B section, has special groove on the base plate of the vapor augmented heatsink of this structure in Figure 1A.
Fig. 3 is the cutaway view of wick structure the 3rd embodiment of trough of belt along the A-A section, has clathrum on the base plate of the vapor augmented heatsink of this structure in Figure 1A.
Fig. 4 A is the cutaway view of multicore wick structure the 4th embodiment of vapor augmented heatsink among Figure 1A along the A-A section.
Multicore wick structure the 4th embodiment of the vapor augmented heatsink of Fig. 4 B shown in being is along the cutaway view of B-B section.
Fig. 5 A is the cutaway view of another multicore wick structure the 5th embodiment of vapor augmented heatsink among Figure 1A along the A-A section.
Fig. 5 B is the cutaway view of multicore wick structure the 5th embodiment of vapor augmented heatsink among Figure 1A along the B-B section.
Fig. 5 C is the cutaway view of multicore wick structure the 5th embodiment of vapor augmented heatsink among Figure 1A along the C-C section.
Fig. 6 A is that vapor augmented heatsink is along the cutaway view of D-D section among Figure 1A, and what illustrate is the capillary wick structure that has liquid reservoirs.
Fig. 6 B is that vapor augmented heatsink is along the cutaway view of B-B section among Figure 1A, and what illustrate is the capillary wick structure that has liquid reservoirs.
Fig. 7 A is that vapor augmented heatsink is along the cutaway view of A-A section among Figure 1A, and what illustrate is the capillary wick structure that has the solid-liquid phase change parts.
Fig. 7 B is that vapor augmented heatsink is along the cutaway view of B-B section among Figure 1A, and what illustrate is the capillary wick structure that has the solid-liquid phase change parts.
Fig. 8 A is the three-dimensional view that has the vapor augmented heatsink of two inverse-T-shaped heat pipe chambers.
Fig. 8 B has the cutaway view of the vapor augmented heatsink of two inverse-T-shaped heat pipe chambers along the A-A section among Fig. 8 A.
Fig. 8 C has the cutaway view of the vapor augmented heatsink of two inverse-T-shaped heat pipe chambers along the B-B section among Fig. 8 A.
Fig. 8 D has the cutaway view of the vapor augmented heatsink of two inverse-T-shaped heat pipe chambers along the C-C section among Fig. 8 A.
Fig. 8 E has the cutaway view of the vapor augmented heatsink of two inverse-T-shaped heat pipe chambers along the D-D section among Fig. 8 A.
Fig. 9 is the front view that has the vapor augmented heatsink of " U " shape heat pipe chamber.
Figure 10 is the front view that has the vapor augmented heatsink of " W " shape heat pipe chamber.
Figure 11 A has the multicore wick structure of vapor augmented heatsink of spherical capillary wick along the cutaway view of A-A section among Figure 1A.
Figure 11 B has the multicore wick structure of vapor augmented heatsink of spherical capillary wick along the cutaway view of B-B section among Figure 1A.
Figure 12-the 14th has the side view of the radiating fin of opening a plurality of geometries and/or yardstick, that comprise at least one vapor augmented heatsink.
Figure 15 and 16 is the side views with radiating fin of otch a plurality of geometries and/or yardstick, that comprise at least one vapor augmented heatsink.
The parts of same Reference numeral TYP in each accompanying drawing.
The specific embodiment
According to Figure 1A, vapor augmented heatsink 100 comprises basal compartment 110, fin chamber 120 and solid fin 130.The thermal source contact site 103 (seeing Figure 1B) of this radiating fin 130 and basal compartment 110 can be processed by for example heat conducting material such as copper or aluminium, and another remainder 102,104 of basal compartment 110 and other chamber can be processed by for example solid materials such as metal, pottery and plastics according to the needs of using.This basal compartment 110 can absorb heat from thermals source 101 (shown in Figure 1B and 1C) such as for example electronic installations.This heat can evaporate the liquid in the basal compartment 110 and produce steam, and this steam can be delivered to other surface of basal compartment 110 and the surface of fin chamber 120 to heat through condensation.The heat that is distributed can be diffused in the radiating fin 130 and final through the air-flow of radiating fin 130 tops convection heat transfer' heat-transfer by convection to surrounding environment.Can on the inwall 102 of fin chamber 120 and basal compartment 110, respectively grid wick structure 119,129 be set.Capillary force through along capillary wick 119,129 can aspirate back the liquid of condensation evaporating area or thermal source contact site 103.Usually, basal compartment 110 all is under the vacuum pressure with fin chamber 120, thereby the inner supporting structure (not shown) can prevent caving in of chamber 110,120.This supporting construction can comprise wick structure (wicking structure).Except reducing thermal-conduction resistance, thermal-convection resistance can reduce through the design of radiating fin.Each solid fin 130 is from two position heat conduction: with the contact 131 of fin chamber 120 and with the contact 132 of basal compartment 110, come for the surface of the convection current on the radiating fin 130 133 provides more even temperature, thereby improve heat radiation.And when air flows downward, the opening 134 that is positioned at the radiating fin bottom can provide auxiliary impact effect also can reduce the back pressure and the pressure drop of air-flow to substrate.Therefore, most of air-flow can pass through radiating fin along substrate, and can before arriving basal compartment 110, not avoid radiator midway.Increasing the baffle plate (not shown) through the side at radiating fin comes steering current can obtain better flow-catheter effect downwards.
For optimize liquid flow and steam flow, can adopt wick structure with spatial variations.Usually, the flow rate of liquid along basal compartment 110 is higher than along the flow rate of liquid of fin chamber 120.The wick structure that is positioned at basal compartment 110 bottoms can comprise the groove structure 140 on the base plate that is arranged on basal compartment 110, thereby can converge liquid to evaporating area 103 along the wicking power of base plate, shown in Fig. 2 A and 2B.Main line 141,145 guiding liquids leave side 146,147.Groove 142,143,144 guiding liquids crossed groove 141 and 145 and inhale liquid to central authorities.Network 119 is placed at top through at this groove structure layer 140, can inhale return to the liquid of condensation in the evaporating area of central authorities.Groove structure 151,152 can be set on inwall replaces grid to use.According to Fig. 3, vertical trench 151 and horizontal channel 152 can be set in fin chamber 120, and horizontal channel 152 and groove structure 140 are set in basal compartment 110.In order to let, clathrum 153 can be set on groove structure 140 along the wicking Li Genggao of basal compartment 110 bottoms.
For heat radiation better, can adopt more complicated multicore structure, the wick structure structure shown in Fig. 4 A and 4B.Because heat distribution is to carry out through the condensation of generation steam, so the liquid of this condensation also can be distributed on the inner surface of chamber 110 and 120.The liquid of this condensation can be through capillary force along the wick structure layer 111 that contact with locular wall 102 and 121 and quilt is inhaled back evaporating area 103.Because heat flux can significantly reduce through thermal diffusion effect, so flow rate of liquid can be relatively low, thereby can use the structure of common core suction, for example grid.When liquid was inhaled more near evaporating area 103, because liquid converges to less disengagement area from big surface area, then mass velocity increased.Therefore, on most surfaces, can only make wick layer 111,121 with common wick structure (for example, grid, groove, sintered powder layer, or foam structure layer) and the flow of liquid suction to evaporating area 103.In addition,, can adopt the structure of higher wicking power, for example multiple layer metal screen grid, groove, powder, foaming structure, or their combination in zone 112,122 near evaporating area.In addition, also can wick structure bridge 113,123 be set in chamber 110,120, let the liquid not be only to flow but just can flow back to evaporating area 103 through short distance with three-dimensional a plurality of liquid flow paths along inner surface.The structure of this wick structure bridge 113,123 (a plurality of liquid flow path wick structure of this three-dimensional) can be the structure of higher wicking power, for example multiple layer metal screen grid, groove, powder, foaming structure, or their combination.These bridges also can combine with the structural column (not shown) provides necessary support function.Vapor stream kinetic energy influences the heat distribution of chamber surface top.Cross the vapor chamber of chamber when vapor stream,, have the very big temperature difference between evaporating area 103 and the condensing surface if very big along the pressure drop of steam flow channel.If adopt wideer vapor chamber and thinner wick structure, can reduce the pressure drop that caused, thus can be in the final condensation temperature at chamber surface place near the temperature at evaporating area 103 places.Therefore, can improve total high heat dispersion.
According to Fig. 5 A, 5B and 5C, another multicore structure comprises the common wick structure layer 111 that is positioned at basal compartment 110 basal surfaces and is positioned at the high wicking power structure sheaf 112 near the zone of evaporating area 103.Can make capillary layer 115 with the structure sheaf of high wicking power, shown in Fig. 5 B round the substrate side.Can also comprise horizontal across substrate and be positioned in the middle of the substrate, perpendicular to the structure bar 116 of another high wicking power of radiating fin 120.High wicking power structure sheaf 115 can be the height of vapor chamber with high wicking power structure bar 116, thereby layer 115 and bar 116 can be used as the top surface and the wick bridge between the basal surface (three-dimensional a plurality of liquid flow path wick structure) of basal compartment 110.The structure bar 114 of another high wicking power can be perpendicular to the capillary bar 116 of the centre that is positioned at substrate across substrate.The height of capillary bar 114 can be lower than the height of chamber, thereby forms the gap 105 that lets steam flow.Capillary layer 115 along side can be guided the condensed fluid around basal compartment 110 sides the end of capillary bar 114,116 into.Capillary bar 114,116 can be shared total matter stream of liquid and inhale back evaporating area 103 to liquid.Similarly, capillary layer 125 can be set along the side of fin chamber 120, and can until the bottom bridge-type and canal formula capillary bar 124 be set, shown in Fig. 5 A in the centre of fin chamber 120, from its top.
According to Fig. 7 A and 7B, solid-liquid phase change parts 118 can be used for preventing the dehydration that the unexpected increase owing to thermal source 101 heat radiations causes.This phase change element 118 can be little container, in this container, solid-liquid phase change material can be housed.Can select phase-change material to be limited to predetermined temperature to the evaporating area temperature specially, thereby let the melt temperature of phase-change material be lower than the maximum permissible temperature of electronic installation and be higher than the normal operating temperature of vapor augmented heatsink 100.When the heat radiation of electronic installation increased suddenly, evaporation rate can increase and the equilibrium temperature of evaporating area can raise.When the temperature of evaporating area reached the melt temperature of phase-change material, phase change element 118 can absorb heat through melting.Therefore, evaporation rate can not raise always, thereby has prevented dehydration.Thereby can be discharged gradually through solidifying again of phase change element 118 when giving liquid when rate of heat dispation reduces the heat absorbed, the equilibrium temperature at evaporating area 103 places can become its normal running (operation) conditions again.
The geometry of foregoing fin chamber 120 and basal compartment 110 is that a list is inverse-T-shaped.In Fig. 8 A to 8E, vapor augmented heatsink comprise one two inverse-T-shaped.The layout of this multicore structure is similar with the layout of single inverse-T-shaped structure.Suppose that thermal source 101 can be installed in the central authorities of the basal compartment 110 of vapor augmented heatsink 100, but the liquid in its heat vaporization chamber and produce steam, and this steam can be delivered to heat other surface and surfaces of two fin chamber of basal compartment through condensation.Can aspirate the liquid of condensation along wick structure layer 111 and 121 through capillary force.When liquid was inhaled more near evaporating area 103, because liquid converges to less disengagement area from big surface area, so mass velocity increased.Therefore, on most surfaces, can adopt, come as capillary layer 111 and 121 and pumping liquid like common wick structure such as grid, groove, sintered powder, foaming structures.In zone 112,122, can adopt the structure of higher wicking power, for example multiple layer metal screen grid, groove, powder, foaming structure or their combination near evaporating area 103.In addition, auxiliary wick bridge 113,123 can also be set between substrate surface and other surface, they provide three-dimensional a plurality of liquid flow paths, thereby it is shorter to let liquid flow back to the travel distance of evaporating area 103.The structure of this wick bridge 113,123 can be the structure with higher wicking power, for example multiple layer metal screen grid, groove, powder, foaming structure or their combination.In addition, round the side of substrate and cross substrate and can increase auxiliary high wicking power parts 114,115,116, strengthen the ability of inhaling back liquid evaporating area 103.Can introduce liquid reservoirs 117 and solid-liquid phase change parts 118 and prevent the dehydration that causes along with the enhancing of the heat-sinking capability of thermal source 101.
Be respectively the heat pipe chamber structure of " U " shape and " W " shape among Fig. 9 and 10, they can be included in the vapor augmented heatsink.Inner multicore structure can be followed the principle that the inverse-T-shaped and two inverse-T-shaped heat pipe chambers of aforesaid list are constructed.
According to Figure 11 A, the multicore wick structure 111 of this vapor augmented heatsink comprises the capillary wick with semi-circular shape 161.
According to Figure 11 B, the multicore wick structure 111 of this vapor augmented heatsink comprises the capillary wick with a plurality of shapes 123,163.
According to Figure 12-14, the radiating fin 130 of this vapor augmented heatsink can comprise at least one opening 171 with a plurality of geometries and/or yardstick.For example in Figure 12, for example, these openings 171 are of similar shape (geometry), and are promptly circular, and have identical yardstick, promptly all are the same sizes.In another example shown in Figure 13, opening 171,172,173 also is of similar shape (geometry), and is promptly circular, but on size (yardstick), is different on the diameter.In addition, in another example shown in Figure 14, opening 171,174,175 has different shape (geometry), i.e. triangle, circle and square, and go up different in size (yardstick).
According to Figure 15 and 16, the radiating fin 130 of this vapor augmented heatsink can comprise at least one otch 181,182,183,184,185 with a plurality of geometries and/or yardstick.For example in Figure 15, for example, this radiating fin 130 comprises a plurality of otch 181,182,183, and they are of similar shape (geometry), and promptly rectangle still is of different sizes (yardstick).In another example shown in Figure 16, this radiating fin 130 comprises a plurality of otch 181,184,185, and they have different shape (geometry), i.e. rectangle, semicircle and quadrant shape, and be of different sizes (yardstick).
A plurality of embodiments have been described in the front, still, be also to be understood that under the situation that does not break away from the spirit and scope of the present invention and can carry out multiple modification.Therefore, other embodiment within the scope of the appended claims.
Claims (10)
1. heat-transfer arrangement; Comprise: at least one comprises the chamber of condensable fluid; The chamber of said condensable fluid has top surface and lower surface; Said lower surface comprises evaporation region, and this evaporation region is configured to be connected in order to evaporate said condensable fluid with thermal source, and the surface aggregation of condensable fluid in said chamber of evaporation condenses; It is characterized in that,
Said heat-transfer arrangement further comprises:
The cored structure layer, this cored structure layer is along the said top surface setting in said chamber; And
The multicore structure layer, this multicore structure layer is along the said lower surface setting in said chamber;
Wherein, the wicking power of said multicore structure layer is greater than the wicking power of the said cored structure layer of the said top surface setting in said chamber, edge; And
The said multicore structure layer that is positioned at said lower surface further comprises two core zones, and the wicking power in core zone that is positioned at said evaporation region is greater than the wicking power in the core zone that is positioned at said evaporation region periphery.
2. heat-transfer arrangement according to claim 1 is characterized in that, the cored structure layer of the said top surface setting in said chamber, edge comprises the grid wick structure.
3. heat-transfer arrangement according to claim 1 is characterized in that, said multicore structure layer comprises at least one in following: metal grill, be formed at lip-deep at least one groove, powder capillary wick and the foam wick core in said chamber.
4. heat-transfer arrangement according to claim 1 is characterized in that, the said multicore structure layer of at least a portion comprises the grid that is arranged on the groove structure.
5. heat-transfer arrangement according to claim 1 is characterized in that, the said multicore structure layer of at least a portion comprises the foam wick core that is arranged on the groove structure.
6. heat-transfer arrangement according to claim 1; It is characterized in that; In the said multicore structure layer that the lower surface in said chamber, edge is provided with, have at least a part to be made up of a plurality of capillary wick, the porosity of these a plurality of capillary wick is lower than the porosity of the cored structure that is arranged on said top surface.
7. heat-transfer arrangement according to claim 6 is characterized in that, the cored structure that has than low porosity comprises: the layer that number of grid increases progressively for said top surface.
8. heat-transfer arrangement according to claim 1 is characterized in that, said multicore structure layer has different porositys or different aperture sizes.
9. heat-transfer arrangement according to claim 1 is characterized in that, the said cored structure layer of the said top surface setting in said chamber, edge and the structure sheaf in the multicore structure layer are same cored structure.
10. heat-transfer arrangement according to claim 1 is characterized in that, the said cored structure layer of the said top surface setting in edge has general wicking power, and has higher wicking power near the zone of said evaporation region.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US38027402P | 2002-05-15 | 2002-05-15 | |
| US60/380,274 | 2002-05-15 | ||
| US10/390,773 US20040011509A1 (en) | 2002-05-15 | 2003-03-19 | Vapor augmented heatsink with multi-wick structure |
| US10/390,773 | 2003-03-19 |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB038167476A Division CN100390488C (en) | 2002-05-15 | 2003-05-15 | Vapor augmented heatsink with multi-wick structure |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101221023A CN101221023A (en) | 2008-07-16 |
| CN101221023B true CN101221023B (en) | 2012-12-05 |
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Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB038167476A Ceased CN100390488C (en) | 2002-05-15 | 2003-05-15 | Vapor augmented heatsink with multi-wick structure |
| CN2008100040427A Expired - Fee Related CN101221023B (en) | 2002-05-15 | 2003-05-15 | Heat transmission device |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB038167476A Ceased CN100390488C (en) | 2002-05-15 | 2003-05-15 | Vapor augmented heatsink with multi-wick structure |
Country Status (8)
| Country | Link |
|---|---|
| US (4) | US20040011509A1 (en) |
| EP (2) | EP1508014A1 (en) |
| JP (2) | JP4427445B2 (en) |
| CN (2) | CN100390488C (en) |
| AU (1) | AU2003233994A1 (en) |
| HK (1) | HK1080543A1 (en) |
| TW (2) | TWI312858B (en) |
| WO (1) | WO2003098141A1 (en) |
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2003
- 2003-03-19 US US10/390,773 patent/US20040011509A1/en not_active Abandoned
- 2003-05-14 TW TW096112053A patent/TWI312858B/en not_active IP Right Cessation
- 2003-05-14 TW TW092113098A patent/TWI293361B/en not_active IP Right Cessation
- 2003-05-15 EP EP03727665A patent/EP1508014A1/en not_active Withdrawn
- 2003-05-15 CN CNB038167476A patent/CN100390488C/en not_active Ceased
- 2003-05-15 CN CN2008100040427A patent/CN101221023B/en not_active Expired - Fee Related
- 2003-05-15 EP EP10185069A patent/EP2317267A3/en not_active Withdrawn
- 2003-05-15 JP JP2004505620A patent/JP4427445B2/en not_active Expired - Fee Related
- 2003-05-15 AU AU2003233994A patent/AU2003233994A1/en not_active Abandoned
- 2003-05-15 WO PCT/GB2003/002086 patent/WO2003098141A1/en active Application Filing
-
2005
- 2005-11-14 US US11/272,145 patent/US7422053B2/en not_active Expired - Fee Related
-
2006
- 2006-03-14 HK HK06103235A patent/HK1080543A1/en not_active IP Right Cessation
-
2008
- 2008-06-09 US US12/135,297 patent/US7650931B2/en not_active Expired - Fee Related
- 2008-11-20 JP JP2008297395A patent/JP2009139083A/en not_active Withdrawn
-
2009
- 2009-12-07 US US12/632,418 patent/US20100078153A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| US20100078153A1 (en) | 2010-04-01 |
| TWI293361B (en) | 2008-02-11 |
| JP2009139083A (en) | 2009-06-25 |
| US20060060330A1 (en) | 2006-03-23 |
| AU2003233994A1 (en) | 2003-12-02 |
| US7650931B2 (en) | 2010-01-26 |
| WO2003098141A1 (en) | 2003-11-27 |
| HK1080543A1 (en) | 2006-04-28 |
| TW200809158A (en) | 2008-02-16 |
| TWI312858B (en) | 2009-08-01 |
| EP2317267A2 (en) | 2011-05-04 |
| TW200427962A (en) | 2004-12-16 |
| CN101221023A (en) | 2008-07-16 |
| CN1668886A (en) | 2005-09-14 |
| US7422053B2 (en) | 2008-09-09 |
| EP1508014A1 (en) | 2005-02-23 |
| JP2005525529A (en) | 2005-08-25 |
| US20040011509A1 (en) | 2004-01-22 |
| US20080236796A1 (en) | 2008-10-02 |
| JP4427445B2 (en) | 2010-03-10 |
| CN100390488C (en) | 2008-05-28 |
| EP2317267A3 (en) | 2011-08-03 |
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